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(11) | EP 0 041 167 B2 |
| (12) | NEW EUROPEAN PATENT SPECIFICATION |
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Expandable polyolefin compositions and polyolefin foam preparation process Verschäumbare Polyolefinzusammensetzungen und Verfahren zur Herstellung von Polyolefinschaum Compositions expansibles de polyoléfines et procédé pour préparer des mousses de polyoléfines |
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[0001] The present invention relates to a process for the preparation of olefin polymer foams, and, in particular, to an extrusion foaming process for olefin polymers using a stability control additive in conjunction with a blowing agent mixture consisting essentially of dichlorodifluoromethane and at least one aliphatic hydrocarbon, or halogenated hydrocarbon, compound having an atmospheric pressure boiling point of from 0°C to 50°C.
[0002] In addition, the present invention also relates to an expandable olefin polymer composition containing the indicated mixed blowing agent system admixed therein.
[0003] It is well known to prepare olefin polymer foams by heat plastifying a normally solid olefin polymer resin, admixing such heat plastified resin with a volatile blowing agent under heat and pressure to form a flowable gel and thereafter extruding the gel into a zone of lower pressure and temperature to expand and cool the gel form the desired solid olefin foam product.
[0004] A problem frequently encountered is that of preventing an unacceptable degree of shrinkage of partially cured foam during the aging or curing period following manufacture. During the "aging" or "curing" period the blowing agent employed is gradually diffusing out of the cells in the foam product and air is gradually diffusing into the cells in place thereof. For example, until very recently only one blowing agent (i.e., 1,2-dichlorotetrafluoroethane) was known or thought to be capable of providing sufficient dimensional stability during the curing period to permit the commercially viable manufacture of low density (e.g., 1-6 pounds per cubic foot or 16 to 96 kg/m3) foams of ethylenic polymer resins.
[0005] More recently, certain technology has been developed in the area of stability control agents in an attempt to permit the obtension of commercially acceptable dimensional stability with a wider range of volatile halogenated hydrocarbon blowing atents. (See, for example, U.S. Patent 3,644,230 and U.S. Patent 4,214,054.) Unfortunately, these techniques, while generally providing low density ethylenic polymer foams having improved dimensional stability, are somewhat limited in terms of the maximum cross-section of the foam articles that can be obtained therewith from a given type of extrusion apparatus. Accordingly, it would be highly desirable to provide an improved extrusion foaming process capable of producing low density olefin polymer foam articles having both relatively large cross-sectional areas (e.g., providing an increase in the maximum achievable foam cross-sectional area which can be obtained with a given extrusion apparatus) and good dimensional stability as well as other desirable foam properties such as, for example, closed cells of small cell size.
[0006] This invention provides a process for preparing closed-cell olefin polymer foam articles having increased maximum achievable cross-sectional areas on a given type or size of extrusion apparatus and having good dimensional stability which comprises heat plastifying a normally solid olefin polymer resin and intimately admixing therewith, under elevated temperature and pressure, a stability control agent and a mixed blowing agent comprising dichlorodifluoromethane and a further blowing agent; and thereafter extruding the resultant mixture into a zone of lower pressure and cooling to form an olefin polymerfoam; characterized in that the olefin polymer is an ethylene homopolymer or a substantially nonneutralized ethylenic copolymer derived from at least 50 weight percent of ethylene and the mixed blowing agent comprises from 50 to 95 weight percent of dichlorodifluoromethane and from 5 to 50 weight percent of an aliphatic hydrocarbon compound, or a halogenated hydrocarbon compound, having an atmospheric pressure boiling point of from 0°C to 50°C, and that the mixed blowing agent has a saturated vapor pressure of less than 32 kg/cm2 but greater than 25 kg/cm2 at 100°C; and that the mixture of the olefin polymer and of the mixed blowing agent is extruded and cooled to form an olefin polymer foam of a density from 36.20 to 43.41 kg/M3.
[0007] The process is particularly well suited for the preparation of closed-cell olefin polymer foamed articles having relatively small or fine cell size and having relatively large cross-sectional areas (e.g., cross-sectional areas in excess of 50 to 60 in2 (322.6 to 387.1 cm2) taken in a plane perpendicular to the direction of extrusion of the foamed article involved). In addition, such process is especially advantageous in that it permits the preparation of such articles without excessive shrinkage during the manufacture thereof and/or during the storage thereof in fresh foam (i.e., partially cured) form. That is, the resulting foamed articles have, in fresh foam form, relatively good ambient temperature (e.g., 21 °C) dimensional stability; typically shrinking to no less than 95, preferably no less than 90 and most preferably no less than 95, percent of their initial foamed volume under such manufacturing and/or storage (e.g., aging or curing) conditions. In addition, such foamed articles also have, in fresh foam form, relatively good elevated temperature stability; typically shrinking to no less than 80, preferably to no less than 85, percent of their original volume during prolonged exposure at 66°C.
[0008] Olefin polymer resins used in the practice of the present invention are ethylene homopolymers such as low, medium or high density polyethylene, and substantially non-neutralized ethylenic copolymers derived from at least 50 weight percent of ethylene, such as substantially non- neutralized ethylene-acrylic acid copolymers. As ethylenic copolymer resin, it is preferable to use a copolymer having an ethylene content above 75 percent by weight. Naturally, blends of two or more of such olefin polymer resins can also be suitably employed in the practice of the present invention.
[0009] Stability control agents suitable for use herein include the long-chain fatty acid/polyol partial esters described in U.S. Patent 3,644,230 as well as higher alkyl amines, fatty acid amides and complete esters of higher fatty acids such as those described in U.S. Patent 4,214,054. Typically, such stability control additives are employed in an amount ranging from 0.1 to 10 weight percent based upon the weight of the olefin polymer employed and preferably they are employed at a level of from 0.5 to 5 weight percent of such olefin polymer resin. In addition to (or in place of) the foregoing stability control additives, there may also be employed for such purpose substantially non-neutralized copolymers of a-olefins with various monoethylenically unsaturated carboxylic acids such as, for example, copolymers of a major portion of ethylene containing copolymerized therewith a minor proportion of a monoethylenically unsaturated carboxylic acid such as acrylic acid, methacrylic acid and the like. (Preferred carboxyl-bearing copolymers for such stability modification include ethylene-acrylic acid copolymers having from 3 to 45, preferably from 15 to 45, weight percent of acrylic acid copolymerized therein.) When such carboxyl-containing copolymers are used, the amount of their usage is not particularly critical so long as a sufficient amount is employed to impart the desired dimensional stability to the resulting olefin polymer foam product. However, as a general rule (a) when the carboxyl-containing polymer contains relatively lower proportions of acid monomer (e.g., from 3 to 15 weight percent based upon such carboxyl polymer) it will typically be employed in relatively larger proportions (e.g., from 40 to 90 weight percent of the total polymer solids), and (b) when such carboxyl polymer contains higher levels of carboxylic acid monomer therein (e.g., from 15 to 45 weight percent based upon the carboxyl polymer) then such carboxyl-containing polymer will typically be used in the range of from 15 to 40 weight percent of the total polymer solids employed in the extrusion foaming process. Naturally, when the olefin polymer to be foamed itself functions as a stability control agent (e.g., substantially non-neutralized copolymers of ethylene and a monoethylenically unsaturated carboxylic acid such as acrylic acid, etc.), the addition of a further stability control agent as a separate additional ingredient is not necessary since in that event such polymer performs the dual function of being both the polymer to be foamed as well as being its own stability control agent.
[0010] The term "substantially non-neutralized" as used herein with reference to carboxyl-bearing polymers is intended to refer to such polymers in which only a small amount (e.g., less than 5 percent and preferably essentially none) of the carboxyl groups therein is neutralized or crosslinked with a metal ion and such term thus excludes those neutralized carboxyl-bearing ethylenic copolymers commonly referred to in the art as ionomers.
[0011] Preferably, the mixed blowing agent system contains from 5 to 40, more preferably from 5 to 35, most preferably from 5 to 25 and especially about 20, weight percent of the indicated 0°C to 50°C boiling point aliphatic hydrocarbon (and/or halogenated hydrocarbon) compound with the remainder of the system being dichlorodifluoromethane. The mixed blowing agent exhibits a saturated vapor pressure at 100°C of greater than 25, but less than 32, kg/cm2. With regard to this mixed blowing agent system, it is to be noted (a) that such system provides an especially desirable balance between maximum achievable cross-section, fine cell size and dimensional stability at both ambient and elevated (e.g., 66°C) temperatures and (b) that the beneficial performance thereof in the present invention is especially suprising in view of the teaching of U.S. Patent 3,657,165 to the effect that mixed blowing agent systems of this type should have 100°C saturated vapor pressur of less than 25 kg/cm2.
[0012] Suitable 0°C to 50°C boiling point aliphatic hydrocarbon and halogenated hydrocarbon compounds for use in the aforementioned mixed blowing agent system include, for example, n-butane, pentane, trichloromonofluoromethane (FC-11), trichlorotrifluoroethane, dichloromonofluoromethane, ethyl chloride and 1-chloropropane. Preferred 0°C to 50°C boiling point aliphatic or halogenated hydrocarbon compounds for use herein include trichloromonofluoromethane and ethyl chloride.
[0013] In practice, the amount of the aforementioned mixed blowing agent system employed in practicing the present invention will vary and will be dictated primarily by the particular foam density sought to be manufactured via such process. However, as a general rule the amount of such mixed blowing agent employed will typically be in the range of from 0.12 to 0.4 gram-mole of the combined mixed blowing agent per 100 grams of the olefin polymer resin to be foamed therewith.
[0014] In addition to the hereinbefore described ingredients, there may also be employed in the practice of the present invention other ingredients or additives which conventionally find applicability in known extrusion foaming processes such as, for example, known nucleating (or cell- size controlling) agents (e.g., talc, clay, mica, silica, titanium oxide, zinc oxide, calcium silicate, metallic salts of fatty acids such us barium stearate, zinc stearate, aluminum stearate, etc.) and wetting agents.
[0015] The following examples, in which all parts and percentages are on a weight basis unless otherwise indicated, are presented as illustrative of the present invention.
Example 1
[0016] The apparatus used in this example is 1% inch screw type extruder having additional zones for mixing and cooling at the end of usual sequential zones forfeeding, melting and metering. An opening for blowing agent injection is provided in the extruder barrel between the metering and mixing zones. At the end of the cooling zone, there is attached a die orifice having an opening of rectan- tached a die orifice having an opening of rectangular shape. The height of the opening is adjustable while its width is fixed at 0.25 inch (0.635 cm).
[0017] Granular polyethylene having a density of 0.921 g/cc and a melt index of 2.3, talcum powder in an amount of 0.7 part by weight per 100 parts by weight of polyethylene, and a stearamide concentrate consisting of 25 percent by weight of Kemamide® S produced by Humko-Sheffield Chemical Company and 75 percent by weight of polyethylene in an amount sufficient to provide a stearamide level of 1.0 part by weight per 100 parts by weight of total resin are uniformly premixed. A small amount of wetting agent is added to facilitate adhesion of the talcum powder to the polymer granules. The mixture is then fed into the extruder through an opening at one end of the feeding zone at an essentially uniform rate of about 10 pounds per hour. The temperatures maintained at the various extruder zones are approximately 140°C in the feeding zone, 180°C in the melting and metering zones and 150°C in the mixing zone.
[0018] A blowing agent comprising dichlorodifluoromethane (F-12) and trichloromonofluoromethane (F-11) and having a composition and rate as shown in Table is injected into the blowing agent injection port. The temperature of the cooling zone is maintained so as to reduce the temperature of the polymer/blowing agent mixture to a uniform temperature of about 108°C. The resulting foam body exiting the die orifice has an ap- proximate!yrectangular cross-section with rounded corners and is conducted away from the die opening.
[0019] The maximum achievable cross-section of foam body is determined by adjusting the die gap opening and observing the quality of the foam produced at various die gap settings.
[0020] At a die gap near that giving the maximum achievable cross-section foam samples are saved to determine dimensional stability and physical properties of the foam. Dimensional stability at ambient temperature is followed with samples having a length of approximately 8 inches and is determined by observing the minimum volume to which such samples shrink at ambient tempera- turefollowing their preparation. Foam samplevol- umes are determined by measuring the volume of water displaced by said foam samples when submerged therein. The results of various runs performed are summarized in Table I below.
[0021] As is seen in Table I, the maximum achievable foam cross-section increases with the level of F-11 in blowing agent while foam dimensional stability at room temperature in general deteriorates with increasing F-11 level. Cell size also increases with the level of F-11, making the foam appear coarse. The data shown in Table I indicate that a blowing agent system containing 10 to 35 percent of F-11 and the remainder thereof being F-12 provided the best balance between increased foam cross-sectional size and the other important properties (e.g., cell size, dimensional stability at both room temperature and 66°C, etc.). Such blowing agent systems have 100°C saturated vapor pressures in the range of from about 31.4 to about 25.5 kg/cm2 and thus are representative of especially preferred embodiments of the present invention.
Example 2
[0022] The same extrusion apparatus used in Example 1 is employed in this example. A polyethylene having a density of 0.921 g/cc and a melt index of 2.0 is employed as the feedstock. Talcum powder is mixed in at 2.0 parts by weight per 100 parts by weight of polyethylene throughout the test of this example. Except for Test No. 11.1, stearamide concentrate was mixed in so that the level of stearamide became one part per 100 parts by weight of total polyethylene. The operating procedure of the extrusion line in this example was essentially the same as in Example 1.
[0023] Blowing agents used in this example are F-12 and its mixtures with ethyl chloride. Table II shows the compositions and the resultant foam properties.
[0024] In Test No. 11.1, absence of stearamide causes the foam produced in this test to be dimensionally unstable. The blowing agent mixtures comprising 10 and 20 percent of ethyl chloride in Test No. 11.2 and 3 have 100°C saturated vapor pressures of about 30 and about 26.8 kg/cm2, respectively, and provide adequate maximum cross-section and dimensional stability. Tests 11.2 and 11.3 thus represent preferred embodiments of the present invention. The blowing agent mixture comprising 30 percent of ethyl chloride (i.e., Test 11.4) has a 100°C vapour pressure of about 24kg/cm2 and provides foam having somewhat less dimensional stability and somewhat coarser cell size than that of Test 11.2 and 11.3. Thus, Test 11.4 does not represent an example of the present invention. Finally, it should be noted that the 40 and 50 weight percent ethyl chloride blowing agent systems (Test 11.5 and 11.6) have 100°C saturated vapor pressures of about 21.6 and 19.5, respectively, and that Tests 11.5 and 11.6 therefore do not represent examples of the present invention.
1. A process for preparing closed-cell olefin polymer foam articles having increased
maximum achievable cross-sectional areas on a given type or size of extrusion apparatus
and having good dimensional stability which comprises heat plastifying a normally
solid olefin polymer resin and intimately admixing therewith, under elevated temperature
and pressure, a stability control agent and a mixed blowing agent comprising dichlorodifluoromethane
and a further blowing agent, and thereafter extruding the resultant mixture into a
zone of lower pressure and cooling to form an olefin polymer foam, characterized in
that the olefin polymer is an ethylene homopolymer or a substantially non-neutralized
ethylenic copolymer derived from at least 50 weight percent of ethylene and the mixed
blowing agent comprises from 50 to 95 weight percent of dichlorodifluoromethane and
from 5 to 50 weight percent of an aliphatic hydrocarbon compound, or a halogenated
hydrocarbon compound, having an atmospheric pressure boiling point of from 0°Cto 50°C,
and that the mixed blowing agent has a saturated vapor pressure of less than 32 kgjcm2 but greater than 25 kg/cm2 at 100°C, and that the mixture of the olefin polymer and of the mixed blowing agent
is extruded and cooled to form an olefin polymer foam of a density from 36.20 to 43.41
kg/m3.
2. The process of Claim 1 wherein the mixed blowing agent consists essentially of
from 5 to 40 weight percent of said aliphatic or halogenated hydrocarbon compound
and from 60 to 95 weight percent of dichlorodifluoromethane.
3. The process of Claim 1 wherein the stability control agent is a partial ester of
a long-chain fatty acid with a polyol, a higher alkyl amine or a fatty acid amide,
a complete ester of a higher fatty acid or a substantially non-neutralized a-olefin-
monoethylenically unsaturated carboxylic acid copolymer.
4. The process of Claim 1 wherein the stability control agent is stearamide.
5. The process of Claim 4 wherein the stearamide is employed in an amount of from
0.1 to 10 weight percent based upon the olefin polymer weight.
6. The process of Claim 1 wherein the aliphatic or halogenated hydrocarbon component
of the mixed blowing agent is ethyl chloride or trichloromonofluoromethane.
7. The process of Claim 1 wherein the aliphatic or halogenated hydrocarbon component
of the mixed blowing agent is trichloromonofluoromethane.
8. The process of Claim 1 wherein the mixed blowing agent is employed in an amount
of from 0.12 to 0.4 gram mole per 100 grams of olefin polymer.
9. An expandable olefin polymer composition comprising an ethylene homopolymer or
a substantially non-neutralized ethylenic copolymer derived from at least 50 weight
percent of ethyl- ne; from 0.12 to 0.4 gram mole per 100 grams of olefin polymer of
a mixed blowing agent system which comprises from 50 to 95 weight percent of dichlorodifluoromethane
and from 5 to 50 weight percent of an aliphatic hydrocarbon compound, or a halogenated
hydrocarbon compound, having an atmospheric pressure boiling point of from 0°C to
50°C which mixed blowing agent has a saturated vapor pressure at 100°C of greater
than 25 kg/cm2 and less than 32 kg/cm2; and a stability control agent in an amount sufficient to prevent the expanded product
ultimately produced from shrinking to less than 85 weight percent of its initial volume
during the manufacture thereof.
1. Procédé pour préparer des articles en mousse de polymère oléfinique à cellules
fermées, ayant des superficies maximales pouvant être atteintes en section transversale,
augmentées, sur un appareil d'extrusion de type ou dimension donné et ayant une bonne
stabilité dimensionnelle, ce procédé consistant à plastifier à chaud une résine de
polymère oléfinique normalement solide et à y introduire en mélange intime, sous température
et pression élevées, un agent régulateur de stabilité en un agent gonflant mixte comprenant
du dichlorodifluorométhane et un autre agent gonflant; et à extruder ensuite le mélange
résultant dans une zone de pression inférieure et à le refroidir pour former une mousse
de polymère oléfinique, caractérisé par le fait que le polymère oléfinique est un
homopolymère d'éthylène ou un copolymère éthylénique essentiellement non-neutralisé
dérivé d'au moins 50% en poids d'éthylène et que l'agent gonflant mixte comprend de
50 à 95% en poids de dichlorodifluorométhane et de 5 à 50% en poids d'un composé hydrocarboné
aliphatique, ou d'un composé hydrocarboné halogéné, ayant un point d'ébullition à
la pression atmosphérique de 0°C à 50°C, et que l'agent gonflant mixte a une tension
de vapeur saturante inférieure à 32 kg/cm2 mais supérieure à 25 kg/cm2 à 100°C; et que l'on extrude et refroidit le mélange de polymère oléfinique et de
l'agent gonflant mixte pour former une mousse de polymère oléfinique d'une masse volumique
de 36,20 à 43,41 kg/m3.
2. Procédé selon la revendication 1, dans, lequel l'agent gonflant mixte est essentiellement
constitué de 5 à 40% en poids du composé hydrocarboné aliphatique ou halogéné et de
60 à 95% en poids de dichlorodifluorométhane.
3. Procédé selon la revendication 1, dans lequel l'agent régulateur de stabilité est
un ester partiel d'un acide gras à longue chaîne avec un polyol, une alkyl amine supérieure
ou un amide d'acide gras, un ester complet d'un acide gras supérieur ou un copolymère
d'une a-oléfine et d'un acide carboxylique monoéthyléniquement insaturé, essentiellement
non neutralisé.
4. Procédé selon la revendication 1, dans lequel l'agent régulateur de stabilité est
le stéaramide.
5. Procédé selon la revendication 4, dans lequel on utilise le stéaramide en une quantité
de 0,1 à 10% en poids par rapport au poids du polymère oléfinique.
6. Procédé selon la revendication 1, dans lequel le composant hydrocarboné aliphatique
ou halogéné de l'agent gonflant mixte est le chlorure d'éthyle ou le trichloromonofluorométhane.
7. Procédé selon la revendication 1, dans lequel le composant hydrocarboné aliphatique
ou halogéné de l'agent gonflant mixte est le trichloromonofluorométhane.
8. Procédé selon la revendication 1, dans lequel on utilise l'agent mixte gonflant
en une quantité de 0,12 à 0,4 molécule-gramme pour 100 grammes de polymère oléfinique.
9. Composition de polymère oléfinique expansible comprenant un homopolymère d'éthylène
ou un copolymère éthylénique essentiellement non neutralisé dérivé d'au moins 50%
en poids d'éthylène; de 0,12 à 0,4 molécule-gramme, pour 100 grammes de polymère oléfinique,
d'un système d'agent gonflant mixte qui comprend de 50 à 95% en poids de dichlorodifluorométhane
et de 5 à 50% en poids d'un composé hydrocarboné aliphatique, ou d'un composé hydrocarboné
halogéné, ayant un point d'ébullition à la pression atmosphérique de 0°C à 50°C, ledit
agent gonflant mixte ayant un tension de vapeur saturante à 100°C supérieure à 25
kg/cm2 et inférieure à 32 kg/cm2; et un agent régulateur de stabilité en une quantité suffisante pour empêcher le
produit expansé finalement produit de se rétracter à moins de 85% en poids de son
volume initial pendant sa fabrication.
1. Verfahren zur Herstellung von Gegenständen aus geschlossenzelligem Olefinpolymerschaum
mit gesteigerten maximal erzielbaren Querschnittsbereichen auf einer Extrusionsvorrichtung
eines vorgegebenen Typs oder Grösse, und mit guter Dimensionsstabilität, welches ein
Wärmeerweichen eines unter Normalbedingungen festen Olefinpolymerharzes und inniges
Vermischen desselben bei erhöhter Temperatur und erhöhtem Druck mit einem Stabilitätssteuermittel
und einem gemischten Treibmittel, welches Dichlordifluormethan und ein weiteres Treibmittel
enthält, und anschliessendes Extrudieren des erhaltenen Gemisches in eine Zone geringeren
Druckes und Abkühlen zur Bildung eines Olefinpolymerschaums umfasst, dadurch gekennzeichnet,
dass das Olefinpolymer ein Ethylen-Homopolymer oder ein im wesentlichen nicht neutralisiertes
Ethylen-Copolymer ist, welches sich von mindestens 50 Gew.% Ethylen herleitet, und
das gemischte Treibmittel 50 bis 95 Gew.% Dichlorodifluormethan und 5 bis 50 Gew.%
einer aliphatischen Kohlenwasserstoff-Verbindung oder einer halogenierten Kohlenwasserstoff-Verbindung
enthält, mit einem Siedepunkt von 0°C bis 50°C bei Atmosphärendruck, und das gemischte
Treibmittel einen Sättigungsdampfdruck von weniger als 32 kg/cm2, jedoch mehr als 25 kg/cm2 bei 100°C aufweist, und das Gemisch des Olefinpolymers und des gemischten Treibmittels
extrudiert und gekühlt wird, um einen Olefinpolymerschaum einer Dichte von 36,20 bis
43,41 kg/m3 zu bilden.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass das gemischte Treibmittel
im wesentlichen aus 5 bis 40 Gew.% der aliphatischen oder halogenierten Kohlenwasserstoff-Verbindung
und 60 bis 95 Gew.% Dichlorodifluormethan besteht.
3. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass das Stabilitätssteuermittel
ein partieller Ester einer langkettigen Fettsäure mit einem Polyol, ein höheres Alkylamin
oder ein Fettsäureamid, ein vollständiger Ester einer höheren Fettsäure oder ein im
wesentlichen nicht neutralisiertes a-Olefin-monoethylenisch ungesättigtes Carbonsäure-Copolymer
ist.
4. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass das Stabilitätssteuermittel
Stearinsäureamid ist.
5. Verfahren nach Anspruch 4, dadurch gekennzeichnet, dass das Stearinsäureamid in
einer Menge von 0,1 bis 10 Gew.% bezogen auf das Gewicht des Olefinpolymers eingesetzt
wird.
6. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die aliphatische oder halogenierte.
Kohlenwasserstoff-Komponente des gemischten Treibmittels Ethylchlorid oder Trichlormonofluormethan
ist.
7. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die aliphatische oder halogenierte
Kohlenwasserstoff-Komponente des gemischten Treibmittels Trichlormonofluormethan ist.
8. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass das gemischte Treibmittel
in einer Menge von 0,12 bis 0,4 g-Mol pro 100 g Olefinpolymer eingesetzt wird.
9. Expandierbare Olefinpolymer-Zusammensetzung, enthaltend ein Ethylen-Homopolymer
oder ein im wesentlichen nicht neutralisiertes Ethylen-Copolymer, welches sich von
mindestens 50 Gew.% Ethylen herleitet, 0,12 bis 0,4g-Mol pro 100 g Olefinpolymer eines
gemischten Treibmittel-Systems, welches 50 bis 95 Gew.% Dichlordifluormethan und 5
bis 50 Gew.% einer aliphatischen Kohlenwasserstoff Verbindung oder einer halogenierten
Kohlenwasserstoff-Verbindung enthält, mit einem Siedepunkt unter Atmosphärendruck
von 0°C bis 50°C, wobei das gemischte Treibmittel einen Sättigungsdampfdruck bei 100°C
von mehr als 25 kg/cm2 und weniger als 32 kg/cm2 aufweist, und ein Stabilitätssteuermittel in einer Menge, die hinreichend mit, um
ein Schrumpfen des letztlich hergestellten expandierten Produkts auf weniger als 85
Gew.% seines anfänglichen Volumens während dessen Bearbeitung zu verhindern.